Steam Reforming of the Bio-Oil Aqueous Fraction in a Fluidized Bed Reactor with in Situ CO2 Capture

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• 作者：Aingeru Remiro ; Beatriz Valle ; Borja Aramburu ; Andr茅s T. Aguayo ; Javier Bilbao ; Ana G. Gayubo
• 刊名：Industrial & Engineering Chemistry Research
• 出版年：2013
• 出版时间：December 4, 2013
• 年：2013
• 卷：52
• 期：48
• 页码：17087-17098
• 全文大小：710K
• 年卷期：v.52,no.48(December 4, 2013)
• ISSN：1520-5045

文摘

The effect of CO₂ capture in hydrogen production by steam reforming of the bio-oil aqueous fraction was studied. The reforming and cracking activity of the adsorbent (dolomite) and the relationship between these reactions and those corresponding to the catalyst (reforming and water gas shift (WGS)) were considered. The experiments were conducted in a two-step system with the first step at 300 掳C for pyrolytic lignin retention. The remaining volatiles were reformed in a subsequent fluidized bed reactor on a Ni/La₂O₃鈥撐?Al₂O₃ catalyst. A suitable balance was stricken between the reforming and WGS reactions, on the one side, and the cracking and coke formation reactions, on the other side, at 600 掳C for catalyst/dolomite mass ratios 鈮?.17. At this temperature and space-time of 0.45 g_catalyst h (g_bio-oil)^鈭?, bio-oil was fully converted and the H₂ yield was around 99% throughout the CO₂ capture step. Catalyst deactivation was very low because the cracking hydrocarbon products (coke precursors) were reformed.